CN103484521A - Method adopting hydro-thermal treatment to facilitate producing ethyl alcohol and lactic acid through kitchen waste - Google Patents
Method adopting hydro-thermal treatment to facilitate producing ethyl alcohol and lactic acid through kitchen waste Download PDFInfo
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- CN103484521A CN103484521A CN201310437655.0A CN201310437655A CN103484521A CN 103484521 A CN103484521 A CN 103484521A CN 201310437655 A CN201310437655 A CN 201310437655A CN 103484521 A CN103484521 A CN 103484521A
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Abstract
The invention discloses a method adopting hydro-thermal treatment to facilitate producing ethyl alcohol and lactic acid through kitchen waste. The kitchen waste is used as raw materials for producing energy sources and chemical products, so that waste is fully utilized while energy-from-waste and recycling utilization of biomass is realized. According to the method, the kitchen waste is subjected to sorting, hydro-thermal treatment and three-phase separation, and then solid waste obtained after the separation is added with microorganisms, so as to be fermented and generate the ethyl alcohol and the lactic acid; waste water obtained after the separation can be reused in a fermentation tank, and residual waste water of the kitchen waste can be purified and then be discharged or reused; grease obtained after the separation can be used for preparing biodiesel after being subjected to the transesterification. According to the invention, the kitchen waste is more thoroughly hydrolyzed as the hydro-thermal treatment technology is adopted; meanwhile, mixed florae are adopted for fermentation to produce the ethyl alcohol, selected cultures are simple and can be easily obtained, the preparation method is simple, the fermentation technology is simple and convenient, the fermentation effect is excellent, and the method is particularly suitable for industrialized application.
Description
Technical field
The invention belongs to the changing food waste process field, be specifically related to a kind of method that changing food waste is produced ethanol and lactic acid.
Background technology
Changing food waste has that water ratio is high, grease and the high characteristics of organic content.Current treatment technology mainly concentrates on oil refining biofuel, producing methane through anaerobic fermentation and ethanol, microorganism fermentative production feed, fertilizer etc.Wherein, biofuel is by transesterification reaction, to make after meal kitchen waste oil is directly separated; And ethanol makes by adding yeast fermentation after the changing food waste saccharification usually again.Patent of invention " a kind of lactic acid bacteriostasis method that is applicable to changing food waste fermentation " (CN101665809B), be in changing food waste, add milk-acid bacteria produce lactic acid realize antibacterial after, add yeast to be fermented.Patent of invention " a kind of changing food waste comprehensive utilization method " (CN102453614B) makes grease biofuel, adopt aspergillus oryzae to mix with S. cervisiae carries out changing food waste and ferments altogether, make ethanol after the distillation of gained water, after fermentation, solid residue is directly as protein fodder.There are the following problems for existing technological method, need specified conditions, high to equipment requirements, do not relate to Pollutant Treatment etc.
At changing food waste, produce in the prior art of ethanol, fermentation condition and bacterial classification are very large on the quality and yield impact of alcohol product, also very high to the requirement of equipment.(ZL03117223.7) under the condition that acid and pressure are arranged, carry out as patent of invention " a kind of method of utilizing the organic waste production ethanol of rich cellulose and hemicellulose ", require equipment acidproof and high pressure resistant.Patent of invention " a kind of method of utilizing changing food waste to produce ethanol " (CN102321722 A) adopts biological bacteria liquid and mixing enzyme preparation cooperative fermentation changing food waste to produce ethanol, but the composition complexity of biological bacteria liquid and mixing enzyme preparation, bacterial classification is difficult for obtaining, collocation method is comparatively loaded down with trivial details, has in actual applications certain difficulty.
Summary of the invention
The present invention is intended to overcome at least to a certain extent problems of the prior art, provide a kind of hydrothermal treatment consists to promote changing food waste to produce the method for ethanol and lactic acid, using changing food waste as the raw material of producing the energy and high value added product, when taking full advantage of refuse, realize energy and the resource utilization of biomass.The present invention simultaneously selects bacterial classification simple and easy to get, is made into mixed bacterial, and for high-efficiency fermenting ethanol, simple process, be particularly suitable for commercial application.
Above-mentioned purpose of the present invention is achieved by following technical solution:
S1. the hydrothermal treatment consists of changing food waste: by after the sorting kitchen waste of collecting, drop in hydrothermal reactor, suitably add according to actual needs water changing food waste is immersed in water fully, then carry out hydrothermal treatment consists.
S2. the changing food waste after hydrothermal treatment consists in step S1 is isolated to the solid changing food waste: the changing food waste after hydrothermal treatment consists is delivered to triphase separator, carry out grease, water, solid three phase separation, obtain the solid changing food waste.
S3. the preparation of ethanol: the solid changing food waste that step S2 is obtained adds water and mixed bacterial to be fermented, and prepares ethanol; Fermentation residue is standby.Concrete steps are to determine whether add water and amount of water according to solid meal kitchen msw water content situation, make solid-to-liquid ratio reach the required scope of ethanol fermentation; Then after adding mixed bacterial, fermented; Centrifugal after fermentation ends, get supernatant liquor and distilled, obtain ethanol, fermentation residue is standby.
S4. the preparation of lactic acid: the fermentation residue that step S3 is obtained is fermented after adding water, calcium carbonate and bacterial classification, centrifugal after fermentation ends, and supernatant liquor is through the lactic acid of purifying to obtain.
Three phase separation described in step S2 is after isolating grease, then separates the water that surpasses the required solid-to-liquid ratio scope of ethanol fermentation according to actual needs, and remaining water and solid refuse enter next step fermentation.
Step S3 is the water ratio situation of the solid changing food waste that obtains according to step S2, determines whether add water and amount of water, makes solid-to-liquid ratio reach the required solid-to-liquid ratio scope of ethanol fermentation.
Mixed bacterial described in step S3 comprises Pichia yeast, fermentation single cell bacterium, aspergillus tubigensis, rhizopus, S. cervisiae and Trichoderma etc.
The described lactic fermentation bacterial classification of step S4 can carry out lactic fermentation at 30 ℃ ~ 50 ℃, and described lactic fermentation bacterial classification is one or more in Wei Si Salmonella, plant lactobacillus and Rhizopus oryzae.
Preferably, in mixed bacterial, the concentration of Pichia yeast, fermentation single cell bacterium, aspergillus tubigensis, rhizopus, S. cervisiae and Trichoderma is 6 * 10
8~ 8 * 10
8individual/mL.
Preferred, each bacterial classification additional proportion of described mixed bacterial is Pichia yeast: fermentation single cell bacterium: aspergillus tubigensis: rhizopus: S. cervisiae: Trichoderma=1-5:1-6:1-4:1-5:1-6:1-6.
Preferred, the add-on of described mixed bacterial is 0.3% ~ 40% of solid meal kitchen garbage weight.
Preferred, in step S3 and step S4, before fermentation, add respectively solid meal kitchen garbage weight 0.1%-20% without the changing food waste after the sorting of hydrothermal treatment consists.Contain a large amount of indigenous microorganisms in changing food waste without hydrothermal treatment consists, can promote the fermentation of changing food waste, improve ethanol and lactic acid yield.
Preferably, the leavening temperature described in step S3 is 20 ℃ ~ 50 ℃, and fermentation time is 20～480 hours.
Preferably, add water in step S3, the volume ratio that makes water and solid changing food waste is 0.5 ~ 15:1.
As preferably, the water added is the kitchen waste water of storing after three phase separation.
As long as it is just passable at carbon, nitrogen phosphate and sulfur, metal ion needs that each spawn culture based component generally meets bacterial classification nutrition, needn't be confined to concrete nutritive ingredient.For handled easily, preferably, the fungies such as Pichia yeast, aspergillus tubigensis, rhizopus, S. cervisiae, Trichoderma adopt potato glucose nutrient agar (being called for short PDA): potato 200g, glucose 20g, agar 15g～20g, distilled water 1000mL, pH nature, 121 ℃ of sterilizing 20min.Fermentation single cell bacterium adopts the YPD substratum: glucose 20g, peptone 20g, yeast extract 10g, distilled water 1000mL, 121 ℃ of sterilizing 20min.
Preferably, in step S4, the calcium carbonate add-on is 1% ~ 10% of fermentation residue weight, and adding the volume ratio of water and fermentation residue after water is 1 ~ 15:1.As preferably, the water added is the kitchen waste water of storing after three phase separation.
Preferably, the leavening temperature described in step S4 is 30 ℃ ~ 50 ℃, and fermentation time is 24 ~ 480 hours.Preferred, described bacterial classification can carry out lactic fermentation at 30 ℃ ~ 50 ℃, and as one or more in the bacterial classifications such as Wei Si Salmonella, plant lactobacillus and Rhizopus oryzae, bacterial classification concentration is 6 * 10
8~ 8 * 10
8individual/mL.As further preferred, the add-on of described bacterial classification is 0.3%～20% of fermentation residue weight.
The purification of lactic acid adopts the conventional precipitator method: will contain calcium lactate fermentation solution and be concentrated into calcium lactate weight concentration 15% at 100 ℃, then slow cooling to 10 ℃ maintain 5 hours gradually, by centrifugal collection calcium lactate; Calcium lactate is dissolved in 90 ℃ of pure water, and controlling the calcium lactate weight concentration is 20%, is cooled to 60 ℃, and adding the vitriol oil is 2 ~ 3 to pH, and stirring simultaneously makes precipitation fully, filters, and the concentrated lactic acid solution obtained of low pressure makes its weight concentration reach 99%.
The sorting of the changing food waste described in step S1 refers to carries out artificial or mechanical sorting by the changing food waste of collection, sorts out the unfermentable materials such as plastics, metal.When the changing food waste moisture content less, need add after water makes changing food waste be immersed in water fully and carry out again hydrothermal treatment consists.Preferably, water and changing food waste volume ratio are 0.5 ~ 15:1.As further preferred, the water added is the kitchen waste water of storing after three phase separation, with saving water resource, realizes resource circulation utilization.
Preferably, in described step S1, changing food waste hydrothermal treatment consists condition is: process 5min～90min for 90 ℃～200 ℃.
Preferred, in step S1, changing food waste carries out hydrothermal treatment consists after adding ammoniacal liquor, adopts pretreatment with agueous Ammonia changing food waste condition gentleer, and reagent is easy to recycle and reuse, Mierocrystalline cellulose and hemicellulose are destroyed less, few to follow-up fermentation adverse influence.The mass ratio of described ammoniacal liquor and changing food waste is 1:4 ~ 20, and the water added and changing food waste volume ratio are 5 ~ 30:1.
Preferably, in step S2, the changing food waste after hydrothermal treatment consists is drained into to triphase separator by spraying quick-fried mode, then standing separation obtains oil phase, solid phase and water.The high temperature of hydrothermal treatment consists can make the lignocellulose fusing in changing food waste, lignocellulose molecular breakdown, degraded.When the unexpected release of high pressure, while producing the quick-fried mechanical force of spray, further broken organic matter, impel the macromolecular substance such as Mierocrystalline cellulose fully to fragment into small molecules, is beneficial to follow-up fermentation.
Preferably, the changing food waste after hydrothermal treatment consists in step S2 is isolated to grease for the preparation of biofuel, the rear storage of kitchen waste water separation that exceeds the required solid-to-liquid ratio scope of ethanol fermentation is standby, and the kitchen waste water of reuse does not carry out purifying treatment.
Compared with prior art, the present invention has following beneficial effect:
1, the present invention adopts mixed bacterial to carry out kitchen waste ethanol fermentation, and the bacterial classification of selecting is simple and easy to get, and collocation method is simple, and zymotechnique is easy, and ferment effect is good, is particularly suitable for commercial application.
2, the novel method of changing food waste energy recycling of the present invention, take full advantage of changing food waste as fermentation substrate, prepares the renewable resource product that ethanol, lactic acid etc. are of many uses, added value is high, and raw material availability is high, can not produce secondary pollution.
3, the novel method of changing food waste energy recycling of the present invention, be converted into liquid fuel and industrial chemicals by changing food waste.The method production cost is low, is a kind of changing food waste recycle approach that applications well is worth that has.
The accompanying drawing explanation
Fig. 1 is that a kind of hydrothermal treatment consists of the present invention promotes changing food waste to produce the process flow sheet of the method for ethanol and lactic acid.
Embodiment
Below in conjunction with specific embodiment, the present invention is further explained, but embodiments of the present invention is not limited in any way.Unless stated otherwise, in embodiment, related reagent, method is this area reagent commonly used and method.
embodiment 1
1, carry out preliminary sorting by collecting the changing food waste of returning, after removing the foreign material that are difficult for fermentation, drop into hydrothermal reactor hydro-thermal storehouse, add the water of 2 times of volumes, at 130 ℃ of lower hydrothermal treatment consists 60min; Open after motor stirs 10min and close.
2, hydrothermal treatment consists after finishing is sprayed changing food waste quick-friedly to triphase separator, isolates grease and moisture solid changing food waste after standing.
3, the moisture solid changing food waste of separating is delivered to fermentor tank, adding the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio was 1:10, then adds 20% mixed bacterial of solid meal kitchen garbage weight, 35 ℃ of bottom fermentations 96 hours.In mixed bacterial, each bacterial classification ratio is Pichia yeast: zymomonas mobilis: black-koji mould: Tokyo rhizopus: S. cervisiae: Li's Trichoderma=1:1:1:1:1:1.After fermentation ends, centrifugal, get supernatant liquor and distill and obtain ethanol.Fermentation residue is as next step lactic acid fermented raw material.
4, add 5% calcium carbonate of weight toward the fermentation residue in lactic acid fermentation tank, and to add the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio be 1:8.Then, add 10% Wei Si Salmonella of solid weight, 37 ℃ of bottom fermentations 108 hours.After fermentation ends, centrifugal, get supernatant liquor conventional precipitation method purification of lactic acid.
Process flow sheet as shown in Figure 1.
embodiment 2
The present embodiment key step is identical with embodiment 1, and distinguish and be in step 1, when changing food waste contains than juicy, after removing the foreign material that are difficult for fermentation, 200 ℃ of lower Direct Hydrothermals processing 10min, the while is not opened agitator motor.Release after hydrothermal treatment consists finishes, when hydrothermal reactor pressure unloads to 1.5atm, spray changing food waste quick-fried to triphase separator, isolates grease after standing, and exceed the water of the required solid-to-liquid ratio scope of ethanol fermentation, makes solid-to-liquid ratio reach 1:15.Remaining solid and water were delivered to fermentor tank, add 40% mixed bacterial of solid weight, 42 ℃ of bottom fermentations 120 hours.
embodiment 3
The present embodiment key step is identical with embodiment 1, and difference is in step 1, adds the water of 10 times of volumes of solid changing food waste; No longer add water in step 3, directly add 40% mixed bacterial of solid weight, 38 ℃ of bottom fermentations 220 hours.Wherein, in mixed bacterial, each bacterial classification ratio is Pichia yeast: zymomonas mobilis: black-koji mould: Tokyo rhizopus: S. cervisiae: Li's Trichoderma=3:6:4:3:6:6.
embodiment 4
The present embodiment key step is identical with embodiment 1, and difference is in step 3, and adding the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio is 1:8, then adds 1% mixed bacterial of solid weight.Wherein, in mixed bacterial, each bacterial classification ratio is Pichia yeast: zymomonas mobilis: black-koji mould: Tokyo rhizopus: S. cervisiae: Li's Trichoderma=5:6:3:5:3:4, and 40 ℃ of bottom fermentations 96 hours.
embodiment 5
The present embodiment key step is identical with embodiment 1, and difference is in step 4, and toward 10% the calcium carbonate that adds fermentation residue and weight thereof in lactic acid fermentation tank, and to add the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio be 1:5.To in embodiment 1, add 10% Wei Si Salmonella of solid weight to change 20% plant lactobacillus into, 40 ℃ of bottom fermentations 90 hours.Other is identical with embodiment 1.
embodiment 6
The present embodiment key step is identical with embodiment 1, and difference is in step 4, and toward 1% the calcium carbonate that adds fermentation residue and weight thereof in lactic acid fermentation tank, and to add the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio be 1:15.To in embodiment 1, add 10% Wei Si Salmonella of solid weight to change 1% mixed strains into, the plant lactobacillus that mixed strains is 1:1:1 by weight ratio, Wei Si Salmonella, Rhizopus oryzae form, 35 ℃ of bottom fermentations 200 hours.
embodiment 7
The present embodiment key step is identical with embodiment 1, and difference is in step 2, after hydrothermal treatment consists, unloads while being depressed into normal pressure, and changing food waste is delivered to triphase separator, carries out grease, water, solid three phase separation after standing.Do not adopt the quick-fried mode of spray that the changing food waste after hydrothermal treatment consists is delivered to triphase separator.
embodiment 8
The present embodiment key step is identical with embodiment 1, and difference is in step 1, and changing food waste drops into after hydrothermal reactor 5% ammoniacal liquor of the water that adds 3 times of volumes and changing food waste quality, at 140 ℃ of lower hydrothermal treatment consists 20min.Other is identical with embodiment 1.
embodiment 9
The present embodiment key step is identical with embodiment 1, and difference is in step 1, and changing food waste drops into after hydrothermal reactor the water that adds 1 times of volume, and 25% ammoniacal liquor of changing food waste quality, at 180 ℃ of lower hydrothermal treatment consists 30min.Other is identical with embodiment 1.
embodiment 10
The present embodiment key step is identical with embodiment 1, and difference is in step 3 and step 4, before ethanol fermentation and before lactic fermentation, add respectively solid meal kitchen garbage weight 20% without the changing food waste after the sorting of hydrothermal treatment consists.Other is identical with embodiment 1.
comparative Examples 1
The present embodiment key step is identical with embodiment 1, and difference is in step 3, and adding the kitchen waste water of the three phase separation of storage to make the solid-liquid volume ratio is 1:10, will in embodiment 1, add 20% mixed bacterial of solid weight to change the Angel Yeast bacterial classification into.Other is identical with embodiment 1.
comparative Examples 2
The present embodiment key step is identical with embodiment 1, and difference is in step 4, will add 10% Wei Si Salmonella of solid weight to change lactobacillus delbrueckii into, 45 ℃ of bottom fermentations 108 hours.Other is identical with embodiment 1.
Ethanol and the lactic acid production of embodiment 1-10 and Comparative Examples 1-2 the results are summarized in table 1.From the results shown in Table 1:
(1) Comparative Examples 1 is used the conventional ethanol fermentation bacterial classification in this area to produce ethanol, and ethanol production is low, illustrates with the bacterial classification of prior art and compares, and the present invention adopts the ferment effect of mixed bacterial good, can significantly improve the output of ethanol.
(2) embodiment 8 and embodiment 9 add ammoniacal liquor before hydrothermal treatment consists, and ethanol and lactic acid production are high; Explanation adds ammoniacal liquor before hydrothermal treatment consists, can improve ferment effect, improves the output of ethanol and lactic acid.
(3) embodiment 10 adds without the changing food waste after the sorting of hydrothermal treatment consists before ethanol fermentation He before lactic fermentation, and ethanol and lactic acid production are high; Illustrate and add the unpasteurized changing food waste that contains a large amount of indigenous bacterial classifications can improve ferment effect, improve the output of ethanol and lactic acid.
(4) Comparative Examples 2 is used this area conventional lactic fermentation bacterial classification lactic acid-fermenting, and lactic acid production is low, illustrates that the lactic fermentation bacterial classification of the present patent application use is more effective than the strain fermentation of available technology adopting, and lactic acid production is high.
The result of table 1 every 100g changing food waste producing and ethanol and lactic acid
| Embodiment | Ethanol production (mL) | Ethanol content % (v/v) | Lactic acid content (g/L) |
| Embodiment 1 | 135 | 8.6 | 59.8 |
| Embodiment 2 | 140 | 8.8 | 60.9 |
| Embodiment 3 | 140 | 8.5 | 61.4 |
| Embodiment 4 | 130 | 8.1 | 61.2 |
| Embodiment 5 | 135 | 8.6 | 65.6 |
| Embodiment 6 | 135 | 8.6 | 67.9 |
| Embodiment 7 | 120 | 6.5 | 52.3 |
| Embodiment 8 | 140 | 9.1 | 68.3 |
| Embodiment 9 | 145 | 10.2 | 68.8 |
| Embodiment 10 | 150 | 10.8 | 70.5 |
| Comparative Examples 1 | 110 | 2.5 | 55.7 |
| Comparative Examples 2 | 135 | 8.6 | 41.2 |
Claims (10)
1. a hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid, it is characterized in that, comprises the steps:
S1. the hydrothermal treatment consists of changing food waste: will carry out hydrothermal treatment consists after the sorting kitchen waste of collection;
S2. isolate the solid changing food waste in the changing food waste after hydrothermal treatment consists from step S1;
S3. the preparation of ethanol: the solid changing food waste that step S2 is obtained adds water and mixed bacterial to carry out alcohol prepared by fermenting, and fermentation residue is standby;
S4. the preparation of lactic acid: the fermentation residue that step S3 is obtained adds water, calcium carbonate and lactic fermentation bacterial classification to be fermented, and prepares lactic acid;
The described mixed bacterial of step S3 is comprised of Pichia yeast, fermentation single cell bacterium, aspergillus tubigensis, rhizopus, S. cervisiae and Trichoderma;
The described lactic fermentation bacterial classification of step S4 can carry out lactic fermentation at 30 ℃ ~ 50 ℃; Described lactic fermentation bacterial classification is one or more in Wei Si Salmonella, plant lactobacillus and Rhizopus oryzae.
2. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, in described mixed bacterial, the concentration of Pichia yeast, fermentation single cell bacterium, aspergillus tubigensis, rhizopus, S. cervisiae and Trichoderma is 6 * 10
8~ 8 * 10
8individual/mL.
3. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 2, it is characterized in that, in described mixed bacterial, each bacterial classification additional proportion is Pichia yeast: fermentation single cell bacterium: aspergillus tubigensis: rhizopus: S. cervisiae: Trichoderma=1-5:1-6:1-4:1-5:1-6:1-6.
4. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, the add-on of mixed bacterial described in step S3 is 0.3% ~ 40% of solid meal kitchen garbage weight.
5. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, in step S3 the fermentation before and step S4 in the fermentation before add solid meal kitchen garbage weight 0.1% ~ 20% without the changing food waste after the sorting of hydrothermal treatment consists.
6. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, the solid meal kitchen msw water content situation obtained according to step S2 in step S3, adding water to make the volume ratio of water and solid changing food waste is 0.5 ~ 15:1, and the condition of described fermentation is 20 ℃ ~ 50 ℃ fermentations 20 ~ 480 hours.
7. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, in step S4, the calcium carbonate add-on is 1% ~ 10% of fermentation residue weight, the volume ratio of water and fermentation residue is 1 ~ 15:1, the condition of described fermentation is 30 ℃ ~ 50 ℃ fermentations 24 ~ 480 hours, and the concentration of described lactic acid fermenting bacteria is 6 * 10
8~ 8 * 10
8individual/mL, the bacterial classification add-on is 0.3%～20% of fermentation residue weight.
8. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, in step S1, the hydrothermal treatment consists condition is 90 ℃～200 ℃ processing 5min～90min; Add ammoniacal liquor before hydrothermal treatment consists, the mass ratio of described ammoniacal liquor and changing food waste is 1:4 ~ 20; After adding water, the volume ratio of water and changing food waste is 5 ~ 30:1.
9. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 1, it is characterized in that, changing food waste after hydrothermal treatment consists in step S1 is isolated to grease for the preparation of biofuel, kitchen waste water determines whether separate, the separated rear storage of waste water that exceeds the required solid-to-liquid ratio scope of fermenting is standby according to the solid-to-liquid ratio situation.
10. a kind of hydrothermal treatment consists promotes changing food waste to produce the method for ethanol and lactic acid according to claim 9, it is characterized in that, the water added in step S3 or step S4 is for storing standby kitchen waste water, and remaining kitchen waste water is discharge or recycling after purifying.
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| CN103695525A (en) * | 2014-01-02 | 2014-04-02 | 华南农业大学 | Method for increasing lactic acid fermentation yield of kitchen waste employing hydro-thermal treatment |
| CN103695526A (en) * | 2014-01-02 | 2014-04-02 | 华南农业大学 | Method for improving alcohol output of kitchen waste by hydrothermal pretreatment |
| CN103710158A (en) * | 2014-01-02 | 2014-04-09 | 华南农业大学 | Method for producing biodiesel by using kitchen wastes |
| CN103710158B (en) * | 2014-01-02 | 2015-01-21 | 华南农业大学 | Method for producing biodiesel by using kitchen wastes |
| CN103695525B (en) * | 2014-01-02 | 2015-07-29 | 华南农业大学 | A kind of hydrothermal treatment consists improves the method for changing food waste lactic fermentation productive rate |
| CN103695526B (en) * | 2014-01-02 | 2015-07-29 | 华南农业大学 | A kind of hydrothermal pretreatment improves the method for changing food waste alcohol production amount |
| CN103865975A (en) * | 2014-03-03 | 2014-06-18 | 同济大学 | Method for producing acetic acid by fermenting kitchen waste |
| CN103865975B (en) * | 2014-03-03 | 2016-01-20 | 同济大学 | A kind of method utilizing changing food waste fermentative production acetic acid |
| CN105618462A (en) * | 2016-01-18 | 2016-06-01 | 董艺 | Multipurpose kitchen garbage treatment system |
| CN107119102A (en) * | 2017-06-05 | 2017-09-01 | 华南农业大学 | A kind of method that utilization kitchen garbage efficiently produces lactic acid |
| CN107142296A (en) * | 2017-06-05 | 2017-09-08 | 华南农业大学 | A kind of method that kitchen garbage efficiently produces ethanol |
| CN107345176A (en) * | 2017-06-05 | 2017-11-14 | 华南农业大学 | A kind of kitchen garbage high-value-use method |
| CN107119102B (en) * | 2017-06-05 | 2020-02-21 | 华南农业大学 | Method for efficiently producing lactic acid by utilizing kitchen waste |
| CN110951789A (en) * | 2019-12-17 | 2020-04-03 | 清华大学深圳国际研究生院 | Kitchen waste treatment method and system |
| CN110951789B (en) * | 2019-12-17 | 2023-07-18 | 清华大学深圳国际研究生院 | Kitchen waste treatment method and system |
| CN112225316A (en) * | 2020-09-17 | 2021-01-15 | 佛山水务环保股份有限公司 | Preparation method of landfill leachate carbon source |
| CN112779299A (en) * | 2021-03-10 | 2021-05-11 | 重庆工程职业技术学院 | Multi-process combined treatment method and system for kitchen waste |
| CN115318810A (en) * | 2022-08-10 | 2022-11-11 | 浙江工业大学 | Kitchen waste disposal method for producing bio-oil and methane by using ethanol-water co-liquefaction coupled anaerobic fermentation |
| CN115318810B (en) * | 2022-08-10 | 2024-05-31 | 浙江工业大学 | Kitchen waste disposal method for producing biological oil and methane by utilizing co-liquefaction coupling anaerobic fermentation of ethanol and water |
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